solubilization purification

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CelLyticTM系列蛋白裂解液

CelLyticTM系列蛋白裂解液
CelLyticTM系列蛋白裂解液
高效率 操作步骤简单,省时 高得率 得率远优于传统冻融或超声法 高活性 温和非变性条件下抽提活性蛋白 高兼容 与蛋白酶抑制剂、鳌合剂、离液剂等很好兼容 抽提的蛋白无需去除CelLyticTM 试剂即可进行下游实验: 亲和纯化 Western blot 凝胶迁移检测 报告基因检测……
566.28 2136.42 566.28 3758.04 2535.39 3938.22
501.93 3320.46
566.28 2084.94 3989.7
527.67 3629.34 5302.44
促销价¥
384.81 2375.80 685.97 2375.80 409.91 1505.79 2651.86 1054.05 1648.00 393.18 1187.90 217.50 711.07 4341.69 368.08 1271.56
哺乳动物细胞和组织裂解
C2978
CelLytic™ M Cell Lysis Reagent
C3228
CelLytic™ MT Cell Lysis Reagent
CE0500 NXTRACT
R0278
CelLytic™ MEM Protein Extraction Kit CelLytic™ NuCLEAR™ Extraction Kit For mammalian tissue or cultured cells RIPA Buffer
P8215
Protease Inhibitor Cocktail for use with fungal and yeast extracts
P8465
Protease Inhibitor Cocktail for use with bacterial cell extracts

包涵体蛋白质复性 纯化

包涵体蛋白质复性 纯化
HCl, Berol 185, glutathione etc)
?Purification factor: ca 2 ?Recovery: 92% of activity ?Concentration factor: ca 5
IEX
Q Sepharose FF
Belew, M. et al. (1994)
1 mM 2- 巯基乙醇 pH 8
在室温等 30-60 分钟
在+4oC 离心 15 分钟 用 0.22 μm 或 0.45 μm
濾膜 过滤
34
准备 HiTrap? Chelating 柱
? 冲洗 5 ml H2O
? 加 0.5 ml 0.5 M NiSO 4
? 冲洗 5 ml H2O ? 用 5-10 ml 20 mM Tris? -HCl,
破碎细胞 ( Disruption of cell )

分离包涵体
(Seperation of inclusion body)

溶解包涵体 (Dissolve inclusion body)

蛋白质产物的构象复原等。 (Recovery of target protein conformation)
2.去垢剂 :如强的阴离子去垢剂 SDS,可以 破坏蛋白内的疏水键, 避免蛋白形成疏水核 心,可以增溶几乎所有的蛋白。但由于 SDS
无法彻底的去除而不允许在制药过程中使用
(研究)。
3.极端pH :可以破坏蛋白的次级键从而增溶蛋 白。如在 pH>9.0 溶解牛生长激素和牛凝乳蛋白 酶包涵体。有些蛋白可以溶解在 60mMHCl 中。
包涵体 :在某些生长条件下,基因工程菌能
积累某种特殊的生物大分子,它们致密地集聚

烧结机专业词汇

烧结机专业词汇

烧结机专业词汇块矿 lump ore粉矿 ore fines矿石混匀 ore blending配矿 ore proportioning矿石整粒 ore size grading返矿 return fines储矿场 ore stockyard矿石堆料机ore stocker匀矿取料机ore reclaimer熔剂flux消石灰 slaked lime活性石灰 quickened lime有机粘结剂organic binder烧结混合料sinter mixture烧结铺底料 hearth layer for sinter烧结 sintering烧结热前沿 heat front in sintering烧结火焰前沿 flame front in sintering渣相粘结slag bonding扩散粘结 diffusion bonding带式烧结机 Dwight-Lloyd sintering machine 环式烧结机 circular traveling sintering machine烧结梭式布料机shuttle conveyer belt烧结点火料 sintering ignition furnace烧结盘 sintering pan烧结锅 sintering pot烧结冷却机sinter cooler带式冷却机 straight-line cooler环式冷却机 circular cooler,annular cooler圆筒干燥机cylinder dryer球磨机ball mill润磨机damp mill混料筒 mixing drum除尘器 dust collector破碎机crusher分级机 classifier烧结机 sintering machine带式冷却机linear cooler烧结 sintering单辊破碎机 single-roller crusher抽风烧结机 downdraft sintering machine选矿设备 mineral processingequipmentb5E2RGbCAP 烧结设备 sintering equipment带冷机 linear cooler带式烧结机 straight line sintering machine 高炉设备 blast furnace equipmentplEanqFDPw 鼓风烧结机 blast sintering machine 高炉 blast furnace单辊破 single-roller crusher 圆筒干燥机cylinder dryer 四辊破 four-roller crusher 四辊破碎机 four-roller crusher布袋除尘器 bag de-dusting collector 球团设备pelletizing equipment 浮选机 flotation machine 圆筒混料机 cylinder mixer成球盘 disc pelletizer 回转窖 rotary kiln 链蓖机chain grate machineDXDiTa9E3dsink drawing 无芯棒拔制sink float separation 重介质选矿sink hole 缩孑Lsinking mill 减径机sinking sizing mill 减径定径机sinter烧结矿sinter burden烧结装料sinter cake 烧结块sinter cooler烧结矿冷却机sinter forging 烧结锻造 sinter green烧结混合物sinter machine 烧结机 sinter ore烧结矿sinter roasting 烧结焙烧sinter skin烧结表面层sintered alloy 烧结合金sintered aluminum powder 烧结铝粉 sintered carbide烧结碳化物sintered compact 烧结体 sintered density 烧结密度 sintered hard alloy烧结硬质合金 sintered metal 烧结金属sintered part烧结零件 sintered piece 烧结零件sintered skeleton 烧结骨架 sintered steel 烧结钢 sintering 烧结sintering activity 烧结活性 sintering belt 烧结带 sintering box 烧结盒 sintering furnace 烧结炉 sintering inhibitor 烧结抑制剂 sintering kinetics 烧结动力学 sintering line 烧结线sintering mix烧结混合物 sintering pan 烧结盘sintering process 烧结法 sintering temperature 烧结温度 sintering zone 烧结带 six fold axis 六次轴 six high mill 六辊式轧机 size deviation 尺寸偏差 size frequency 粒度频度 size precision 尺寸精确度 sized ore分级矿石 sizing 筛分 sizing mill 定径机 skeleton 骨架skeleton pattern 骨架模型 skelp mill有缝管毗机skew rolling 斜轧 skew table斜辊车昆道 skid移送机 skid pipe炉底滑管 skid rail炉底滑管 skim 泡沫 skim gate挡渣浇口 skimmer撇渣器 skimming 除渣 skimming hole 撇渣口 skin hole表面气孑L skin mill平整机 skin rolling 平整 skin shrinkage 表皮收缩 skip料车skip hoist料斗卷扬机 skip welding 跳焊 skip winch 料车卷杨机 skull结壳 skutterudite 方钻矿slab扁钢坯扁钢锭slab caster板努铸机slab conditioning 板彭面加工slab ingot 扁锭slab mill板捧轧机slab packet 扁纽slab shears板鹏断机slack粉炭slack coal 粉炭slack quenching 不完全淬火slacking down 消弱slag炉渣slag action炉渣侵蚀slag bath 渣浴slag brick 渣砖slag car渣罐车slag cement炉渣水泥slag composition 炉渣组成slag dump 废渣堆slag formation 造渣slag former 造渣齐Uslag free tapping 无渣出钢slag granulation 炉渣粒化slag hammer 除渣锤slag hole 出渣口slag inclusion 夹渣slag ladle 渣罐slag losses渣中金属损失slag melting furnace 炉渣熔炼炉slag notch 出渣口slag notch cooler 出渣口冷却箱slag pit 渣坑slag pocket 沉渣室slag practice 造渣法slag pumice 渣浮石slag resistance 抗渣性slag runner 渣沟slag running off 排渣slag sand炉渣砂slag skimmer 撇渣器slag tapping 出渣slag thimble 渣罐slag trap集渣器slag trough 渣沟slag tuyere 渣口小套slag tuyere cooler 渣口冷却套 slag wool 渣棉slag yield出渣率slagging渣化。

反胶束萃取技术及应用

反胶束萃取技术及应用

反胶团萃取体系
单一反胶团体系: 单一反胶团体系[1] 的表面活性剂有阴离子型、阳离子 型和非离子型。研究最多的是AOT/ 异辛烷体系, 该体 系结构简单而稳定, 反胶团体积相对较大,适用于等电 点较高、相对分子质量较小的蛋白质的分离; AOT:丁二酸- 2 - 乙基已基酯磺酸钠 常用的阳离子型表面活性剂有TOMAC、十六烷基三 甲基溴化铵(CTAB) 、二辛基二甲基氯化铵等季铵盐。
反胶束的制备
溶解法:对非水溶性的蛋白质可用此法。将含 有反胶束的有机溶液与蛋白质固体粉末一起搅 拌时蛋白质进入反胶束中(需较长的时间)。
ቤተ መጻሕፍቲ ባይዱ
提取胞内酶及胞外酶
Rahaman 等[5] 用AOT/ 异辛烷体系, 从发酵液中 回收了碱性蛋白酶, 酶的提取率可达50 %; Giovenco 等[6]用CTAB/ 己醇- 辛烷体系提取和纯化棕色固氮 菌的胞内脱氢酶: 完整的细胞在表面活性剂的作用下 溶解, 析出酶进入反胶团的“水池”中, 再通过选取 适当的反萃取方法, 回收高浓度的活性酶。
反胶团萃取体系
混合反胶团体系: 这是指两种或两种以上表面活性剂构成的体系。 一般说来, 混合表面活性剂反胶团体系对蛋白质有更 高的分离效率。 例如将AOT 与二- (2 - 乙基己基)磷酸(DEHPA) 构成的 混合体系, 可萃取相对分子质量较大的牛血红蛋白, 萃 取率达80 %。 非离子表面活性剂的加入可使反胶团变大, 从而可萃 取相对分子质量更大的蛋白质。
对一个由水、表面活性剂和非极性有机溶剂构 成的三元系统, 共存相可用三元相图表示。 由下页中图2是水-AOT- 异辛烷系统的相图示 例, 从图2 可知, 能用于蛋白质分离的仅是位于 底部的两相区, 在此区内的三元混合物分为平 衡的两相: 一相是含有极少量有机溶剂和表面 活性剂的水相; 另一相是作为萃取剂的反胶束 溶液。

重组人表皮生长因子在毕赤酵母X33中的构建、表达和纯化

重组人表皮生长因子在毕赤酵母X33中的构建、表达和纯化

重组人表皮生长因子在毕赤酵母X33中的构建、表达和纯化高云鹏;赵雨;王新宇;白雪媛;王佳雯【摘要】在毕赤酵母X33中表达人表皮生长因子并纯化,对表皮生长因子(EGF)进行密码子优化,构建pPICZa A-EGF真核表达质粒,转化X33感受态细胞;利用抗性筛选以及PCR鉴定阳性菌株.经过甲醇诱导和镍柱纯化,聚丙烯酰胺凝胶电泳检测蛋白分泌表达情况.成功构建了表达pPICZa A-EGF真核表达质粒,转入X33中获得阳性菌株,成功诱导蛋白分泌表达并纯化.在毕赤酵母X33中成功表达人表皮生长因子,纯化后纯度为80%,收率为5.8 mg/L.【期刊名称】《科学技术与工程》【年(卷),期】2018(018)017【总页数】4页(P141-144)【关键词】表皮生长因子;毕赤酵母;蛋白表达;纯化【作者】高云鹏;赵雨;王新宇;白雪媛;王佳雯【作者单位】长春中医药大学中医药与生物工程研究开发中心,长春130117;长春中医药大学中医药与生物工程研究开发中心,长春130117;长春中医药大学中医药与生物工程研究开发中心,长春130117;长春中医药大学中医药与生物工程研究开发中心,长春130117;长春中医药大学中医药与生物工程研究开发中心,长春130117【正文语种】中文【中图分类】Q786表皮生长因子(EGF)首次从成熟小鼠的颌下腺中分离出来[1]。

而人的肾脏、十二指肠、胰腺、肝脏以及乳腺中都发现了人表皮生长因子(hEGF)存在[2, 3]。

hEGF是包含有53个氨基酸残基,具有三个二硫键的6.2 kDa大小的多肽。

EGF能够与表皮生长因子受体(EGFR)结合并使其激活,活化后的EGFR由单体转化为二聚体并发生自磷酸化,进一步激活下游包括MAPK/Akt和JNK在内的一系列通路,诱导细胞增殖[4]。

hEGF刺激皮肤、角膜、肺、器官以及胃肠道表皮细胞的增殖和分化。

hEGF同时能够促进角质细胞的生长和迁移,提高成纤维细胞和胚胎细胞的增殖[4,5]。

沙门氏菌发酵液纯化流程

沙门氏菌发酵液纯化流程

Purification Process of Salmonella Fermentation BrothThe purification of Salmonella fermentation broth involves a meticulous series of steps to isolate and purify the desired products. This process ensures the removal of impurities, concentration of the target compounds, and their subsequent purification to obtain a high-quality product. Here's an overview of the purification process for Salmonella fermentation broth:Harvesting and Clarification: The first step involves harvesting the fermentation broth, which typically contains a mixture of cells, metabolites, and other impurities. Clarification is then performed to remove larger particles and debris by centrifugation or filtration methods.Extraction: Following clarification, the broth is subjected to extraction to separate the desired compounds from the aqueous phase. This step often involves the use of solvents to extract the target molecules based on their solubility properties.Solvent Removal: Once the extraction is complete, the solvent is removed, leaving a concentrated mixture of the target compounds. This can be achieved through evaporation, distillation, or other suitable techniques.Purification: The concentrated mixture is then further purified to remove any residual impurities. Chromatography techniques, such as column chromatography or preparative high-performance liquid chromatography (HPLC), are commonly used for this purpose. These methods allow for the separation of individual components based on their physical or chemical properties.Drying and Storage: Finally, the purified product is dried to remove any remaining moisture and stored properly to maintain its stability and quality.It's important to note that the purification process for Salmonella fermentation broth may vary depending on the specific compounds being targeted and the desired purity level. Additionally, strict quality control measures are essential throughout the process to ensure the safety and efficacy of the final product.沙门氏菌发酵液纯化流程沙门氏菌发酵液的纯化涉及一系列精心设计的步骤,以分离和纯化所需的产品。

蛋白粉的提取工艺流程

蛋白粉的提取工艺流程

蛋白粉的提取工艺流程英文回答:Protein powder is a popular dietary supplement that is widely used by athletes, fitness enthusiasts, and individuals looking to increase their protein intake. The extraction process of protein powder involves several steps to obtain a high-quality product.1. Source Selection: The first step in the extraction process is selecting the source of protein. Common sources include whey, casein, soy, and pea. Each source has its own unique properties and nutritional profile.2. Pre-Treatment: Once the protein source is selected, it undergoes pre-treatment to remove any impurities or unwanted components. This may involve processes like filtration, centrifugation, or precipitation to separate the protein from other substances.3. Solubilization: The protein is then solubilized to make it easier to extract. This can be done by adding a solvent or using enzymatic hydrolysis to break down the protein into smaller, soluble peptides.4. Extraction: The solubilized protein is extracted using various methods depending on the source. For example, whey protein is typically obtained through filtration processes like microfiltration or ultrafiltration. Soy protein, on the other hand, may require alkaline extraction followed by precipitation.5. Concentration: After extraction, the proteinsolution is concentrated to increase the protein content. This can be achieved through processes like evaporation or membrane filtration.6. Purification: To ensure the purity of the protein powder, further purification steps may be employed. This can involve techniques like chromatography or ion exchange to remove any remaining impurities or contaminants.7. Drying: The final step in the extraction process is drying the purified protein solution to obtain a powder form. This can be done through methods like spray drying or freeze drying, which remove the water content while preserving the protein's integrity.Overall, the extraction process of protein powder involves source selection, pre-treatment, solubilization, extraction, concentration, purification, and drying. Each step is crucial in obtaining a high-quality protein powder with desirable nutritional and functional properties.中文回答:蛋白粉的提取工艺流程包括以下几个步骤:1. 原料选择,首先需要选择蛋白粉的原料。

天然药化专业英语词汇(一)

天然药化专业英语词汇(一)

天然药化专业英语词汇(一)
天然药化专业英语词汇
天然药化是研究天然药物的化学成分及其化学性质,探索其生物活性
以及制备天然药物和药物前体的科学。

以下是天然药化专业英语词汇:
1. Natural products:天然产物,指来源于自然界的生物分子,包括
植物、动物和微生物等。

2. Phytochemistry:植物化学,指对植物中的生物活性成分进行分离、鉴定、结构解析和制备药物的研究。

3. Bioactivity:生物活性,指物质对生物体产生的影响,如生长、
繁殖和代谢等。

4. Secondary metabolites:次生代谢产物,指植物、菌物和动物等
分泌出的次生代谢产物,如生物碱、黄酮类、苷类和酚酸类等。

5. Isolation:分离,指从混合物中分离出单一物质或混合物。

6. Purification:纯化,指将混合物中的目标物分离出来,并去除不
需要的杂质。

7. Structural elucidation:结构解析,指通过实验手段确定化合物
的分子结构。

8. Chemical modification:化学修饰,指化合物分子中的化学反应,如酯化、还原、氧化和脱水等。

9. Biosynthesis:生物合成,指生物体内的化学反应活动,如植物合成天然产物。

10. Pharmacology:药理学,指药物对生物体产生的药理效应,包括药效、毒理和药代动力学等。

以上词汇是天然药化专业不可或缺的基础词汇,掌握这些词汇能让我们更好地理解和研究天然药化科学的内容。

同时,建议在学习这些词汇时,结合实际案例和文献进行学习,加强对这些词汇的理解和应用能力。

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Solubilization,purification and reconstitution of Ca 2+-ATPase from bovine pulmonary artery smooth muscle microsomes by different detergents:Preservation of native structure and function of the enzyme by DHPCAmritlal Mandal,Sudip Das,Tapati Chakraborti,Pulak Kar,Biswarup Ghosh,Sajal Chakraborti *Department of Biochemistry and Biophysics,University of Kalyani,Kalyani 741235,West Bengal,India Received 30June 2005;received in revised form 21September 2005;accepted 27September 2005Available online 19October 2005AbstractThe properties of Ca 2+-ATPase purified and reconstituted from bovine pulmonary artery smooth muscle microsomes {enriched with endoplasmic reticulum (ER)}were studied using the detergents 1,2-diheptanoyl-sn-phosphatidylcholine (DHPC),poly(oxy-ethylene)8-lauryl ether (C 12E 8)and Triton X-100as the solubilizing agents.Solubilization with DHPC consistently gave higher yields of purified Ca 2+-ATPase with a greater specific activity than solubilization with C 12E 8or Triton X-100.DHPC was determined to be superior to C 12E 8;while that the C 12E 8was determined to be better than Triton X-100in active enzyme yields and specific activity.DHPC solubilized and purified Ca 2+-ATPase retained the E1Ca ÀE1*Ca conformational transition as that observed for native microsomes;whereas the C 12E 8and Triton X-100solubilized preparations did not fully retain this transition.The coupling of Ca 2+transported to ATP hydrolyzed in the DHPC purified enzyme reconstituted in liposomes was similar to that of the native micosomes,whereas that the coupling was much lower for the C 12E 8and Triton X-100purified enzyme reconstituted in liposomes.The specific activity of Ca 2+-ATPase reconstituted into dioleoyl-phosphatidylcholine (DOPC)vesicles with DHPC was 2.5-fold and 3-fold greater than that achieved with C 12E 8and Triton X-100,respectively.Addition of the protonophore,FCCP caused a marked increase in Ca 2+uptake in the reconstituted proteoliposomes compared with the untreated liposomes.Circular dichroism analysis of the three detergents solubilized and purified enzyme preparations showed that the increased negative ellipticity at 223nm is well correlated with decreased specific activity.It,therefore,appears that the DHPC purified Ca 2+-ATPase retained more organized and native secondary conformation compared to C 12E 8and Triton X-100solubilized and purified preparations.The size distribution of the reconstituted liposomes measured by quasi-elastic light scattering indicated that DHPC preparation has nearly similar size to that of the native microsomal vesicles whereas C 12E 8and Triton X-100preparations have to some extent smaller size.These studies suggest that the Ca 2+-ATPase solubilized,purified and reconstituted with DHPC is superior to that obtained with C 12E 8and Triton X-100in many ways,which is suitable for detailed studies on the mechanism of ion transport and the role of protein–lipid interactions in the function of the membrane-bound enzyme.D 2005Elsevier B.V .All rights reserved.Keywords:Ca 2+-ATPase;Endoplasmic reticulum;Bovine pulmonary artery smooth muscle microsome;Liposome;DHPC;C 12E 8;Triton X-100;DOPC;FCCP1.IntroductionChanges in the intracellular Ca 2+concentration [(Ca 2+)i ]regulate the contraction–relaxation cycle of smooth muscle [1].Plasma membrane Ca 2+-ATPase and endoplasmic reticular (ER)Ca 2+-ATPase play important roles in counteracting an increase in [(Ca 2+)i ]in smooth muscle caused by different agonists [1].Recent research provided evidence suggesting that the ER Ca 2+-ATPase is one of the intrinsic Ca 2+transport membrane protein,which is involved in Ca 2+uptake in the suborganelle [2].Three genes of ATP2A1,ATP2A2and ATP2A3encode three types of SERCA protein.SERCA 1,0304-4165/$-see front matter D 2005Elsevier B.V .All rights reserved.doi:10.1016/j.bbagen.2005.09.013Abbreviations:ER,endoplasmic reticulum;SR,sarcoplasmic reticulam;DHPC,1,2-diheptanoyl-sn-phosphatidylcholine;C 12E 8,poly(oxy-ethylene)8-lauryl ether;DOPC,dioleoyl-phosphatidylcholine;DTT,D,L-1,4-dithiothreitol;HBPS,Hank’s buffered physiological saline;MOPS,3-(N -morpholino)propa-nesulphonic acid;TBS,tris-buffered saline;EGTA,ethylene glycol bis(2-aminoethyl ether)-N,N,N V ,N V -tetraacetic acid;PMSF,phenylmethylsulfonyl fluoride;DFBAPTA,5-5V difluoro derivative of 1,2-bis(o-aminophenox-y)ethane-N,N,N V ,N V ,tetraacetic acid;CD,circular dichroism;FCCP,carbonyl-cyanide-p -trifluoromethoxyphenylhydrazone*Corresponding author.Tel.:+919831228224;fax:+913325828282.E-mail address:saj _chakra@ (S.Chakraborti).Biochimica et Biophysica Acta 1760(2006)20–31SERCA2and SERCA3and alternative splicing of the three primary transcripts gives rise to at least nine SERCA isoforms with different functions[3–7].SERCA2b isoform having mol mass of¨115kDa[8]is the principal form of the Ca2+-ATPase in smooth muscles and appears to represent a generic‘‘ER’’form of the Ca2+-ATPase[9].Ca2+-ATPase couples the transport of2mol of Ca2+across the ER membrane with the hydrolysis of1mol of ATP and a conformational change accompanies the reaction cycle[10–12].To elucidate fully the structure and function of Ca2+-ATPase,and particularly the role of lipidÀprotein interactions in the conformational changes that accompany ion transloca-tion,it is necessary to isolate the protein and separate it from other membrane constituents.The most successful approach so far involves the use of detergents for solubilization[12–19] and for reconstitution into defined lipids[20–29].A major challenge in the solubilization and reconstitution of membrane proteins is the choice of a detergent that preserves the native protein structure and biological function.Nonionic detergents such as C12E8and Triton X-100have been employed for the solubilization and purification of Ca2+-ATPase from sarcoplas-mic reticulum(SR)[12,13,16,17].These procedures have produced varied results in terms of active enzyme yield, specific activity and formation of phosphorylated enzyme. Reconstitution of membrane proteins into liposomes provides a powerful tool in structural as well as functional areas of membrane protein research[24,30].It has been shown that in some systems,for example,sarcoplasmic reticulum,the nature of the detergent used for reconstitution is a key factor in determining the properties of the reconstituted system[30].In some membrane preparations,C12E8and Triton X-100have emerged suitable detergents for optimizing the recovery of membrane bound enzymes[18,24,29–35].To the best of our knowledge,reconstitution of pulmonary artery smooth muscle microsomal(enriched with ER)Ca2+-ATPase into defined lipids has not been performed with any study based on these detergents.A short chain phospholipid detergent,DHPC has been described by Kessi et al.[30]and Shivanna and Rowe [35]for solubilizing membrane proteins[35].They showed that DHPC is a better solubilizing agent for a variety of membrane proteins,while retaining their maximal native activity.We have applied DHPC for solubilization,purification and reconstitution of Ca2+-ATPase from bovine pulmonary artery smooth muscle microsomes.In this present communication,we compared the effectiveness in solubilizing and purifying Ca2+-ATPase using DHPC with that prepared by using C12E8and Triton X-100by studying simultaneous measurements of Ca2+-ATPase activity and ATP dependent Ca2+uptake.Furthermore, detailed comparison of the DHPC,C12E8and Triton X-100 purified preparations was made by tryptophan fluorescence and also by circular dichroism spectroscopy.Reconstitution of Ca2+-ATPase into dioleoylphosphatidylcholine(DOPC)using DHPC,C12E8and Triton X-100were performed and the resulting activities were compared.Our results demonstrate that the DHPC purified and reconstituted Ca2+-ATPase into DOPC gives a higher activity compared to that of C12E8and Triton X-100purified preparations.To our knowledge,this is the first report for purification and reconstitution of Ca2+-ATPase of bovine pulmonary artery smooth muscle microsomal Ca2+-ATPase into DOPC using the short-chain phospholipid detergent DHPC.2.Materials and methods2.1.MaterialsDHPC and DOPC were obtained from Avanti Polar Lipids.C12E8,Triton X-100,Tris-ATP,PMSF,sucrose,DTT,CaCl2,rotenone,NADPH,AMP,p-nitrophenylphosphate,p-nitrophenol,cytochrome c,EGTA,Reactive Red120-agarose,FCCP and horseradish peroxidase conjugated secondary antibody were purchased from Sigma Chemical Co.,St.Louis,MO,USA.Sephadex G-100was procured from Pharmacia,Upsala,Sweden.Bio-Beads SM-2(average pore diameter90A˚)was purchased from Bio-Rad,California,USA.DFBAPTA and Fura Red,tetraammonium salt were the products of Molecular Probes,OR, USA.BCA protein assay kit was obtained from Pierce,Rockford,Illinois, USA.Control SERCA2b and its polyclonal antibody were supplied by Dr. Jonathan Lytton,University of Calgary,Calgary,Canada.All other chemicals used were of analytical grade.2.2.Methods2.2.1.Microsome preparationBovine pulmonary artery collected from slaughterhouse was washed several times with Hank’s buffered physiological saline(HBPS)(137mM NaCl, 1.1mM MgCl2, 4.69mM KCl, 3.7mM HEPES buffer,11mM Glucose,pH7.4)and kept at4-C.The washed pulmonary artery was used for further processing within1h after collection.The intimal and serosal (external)layers were removed and the tunica media,i.e.,the smooth muscle tissue was collected and used for the present studies[36].The smooth muscle tissue was characterized by histology with eosin–hematoxylin stain in a light microscope[37].Microsomes enriched with the ER from the smooth muscle tissue were prepared by following the procedure described by Chakraborti et al.[38].2.2.2.Characterization of microsomes by the assay of marker enzymesRotenone-insensitive cytochrome c reductase activity was measured as previously described[39].Cytochrome c oxidase was assayed by the procedure of Wharton and Tzagoloff[40].Acid phosphatase activity was determined at pH5.5using p-nitrophenylphosphate as the substrate[41].Release of Pi from 5V AMP,an index of5V-nucleotidase activity,was determined by the method of Chen et al.[42].2.2.3.Determination of proteinProtein concentration was estimated by the Pierce Micro BCA protein assay kit(Pierce,Rockford,Illinois,USA)by following the procedure of Smith et al.[43]using bovine serum albumin(BSA)as the standard.2.2.4.Solubilization and Purification of Ca2+-ATPase from the smooth muscle microsomeAll buffers used contain1mM PMSF,1A M pepstatin and10A M leupeptin unless stated otherwise.All purification steps were performed at 4-C.2.2.4.1.Solubilization of microsomal vesicles.The freshly prepared microsomes were solubilized on ice with detergents(DHPC,C12E8and Triton X-100)as described by Kessi et al.[30]with some modifications.Briefly,200 mM stock solutions of detergents in solubilization buffer(50mM Tris–HCl,1 M KCl,20%glycerol,1mM DTT,pH7.5)were added to freshly prepared microsomes to the desired final detergent concentration at a constant microsomal vesicle protein concentration of6mg/ml in the same buffer. Overall,the detergent/protein ratio appears to be1:1for Triton X-100;1:0.9forA.Mandal et al./Biochimica et Biophysica Acta1760(2006)20–3121C12E8;and1.5:1for DHPC,which have been determined by us to be optimum for enzyme solubilization and optimum activity.Unless stated otherwise,microsomal vesicles were solubilized at0-C by drop-wise addition of stock detergent solution with vortex-mixing for60s. Solubilization continued on ice for30min with intermittent mixing.Final concentrations of each of the detergents were varied between0and50mM. The solubilization mixture was centrifuged at105,000Âg in an Ultracentrifuge (Beckman,USA)at4-C for25min.The enzyme activity was determined in both the supernatants and the pellets[30].2.2.4.2.Reactive Red120-agarose chromatography.Microsomes were solubilized with the buffer A(50mM Tris–HCl buffer,pH7.5,0.5 mM MgCl2,2mM DTT,20%glycerol,0.5mM EGTA and50A M CaCl2) containing the respective detergents(DHPC or C12E8or Triton X-100).During the solubilization,the optimal detergent concentrations were used of20mM DHPC or10mM C12E8or10mM Triton X-100on the basis of the solubilization data obtained from the present study.Protein concentration was kept at4.0–4.5mg/ml and loaded on to a Reactive Red120-agarose column(1.5Â10cm)equilibrated with buffer A containing either of the detergents ata flow rate of6ml/h[44].Proteins were next eluted with step gradient of NaCl(0.5and2M)in buffer A containing the final concentration of the detergents,with the flow rate of12ml/h.Proteins were monitored spectrophotometrically at280nm and assayed for Ca2+-ATPase activity.The enzyme was eluted with0.5M NaCl.The fractions with maximum Ca2+-ATPase activity from several runs were pooled and concentrated by Amicon ultrafiltration cell with YM10membrane(Mr cut off=10kDa).The concentrated pool was adjusted to contain100mM KCl and400A g/ml phosphatidylcholine.2.2.4.3.Sephadex G-100chromatography.The concentrated material (2ml)obtained after Reactive Red120-agarose chromatography was loaded on a Sephadex G-100column(2.3Â92.5cm)equilibrated with buffer A containing100mM KCl with the final concentration of detergents 20mM DHPC,10mM C12E8and10mM Triton X-100and eluted at a flow rate of9ml/h.Proteins were monitored spectrophotometrically at280 nm.All fractions were assayed for Ca2+-ATPase activity and supplemented with400A g/ml phosphatidylcholine.Fractions with highest Ca2+-ATPase activity from several runs were pooled and concentrated by Amicon ultrafiltration cell with YM10membrane(Mr cut off=10kDa).The pooled concentrated fractions with Ca2+-ATPase activity were stored under liquid nitrogen.2.2.5.SDS-polyacrylamide gel electrophoresisSodium dodecyl sulfate(SDS)-polyacrylamide gel electrophoresis was performed according to the procedure of Laemmli[45]using a minigel Protean II apparatus(Bio-Rad,USA).The protein bands were visualized by silver staining methods[46].2.2.6.Identification of purified Ca2+-ATPase by Western immunoblotCa2+-ATPase purified from the smooth muscle microsomal suspension was identified by western immunoblot,performed by following the method of Towbin et al.[47]using the polyclonal anti-SERCA2b as the primary antibody [48].Horseradish peroxidase conjugated goat anti-rabbit IgG was used as the secondary antibody.The nitrocellulose membrane was developed with4-chloro-1-naphthol(0.2mM).2.2.7.Reconstitution of DHPC,C12E8and Triton X-100purified Ca2+-ATPase into DOPCCa2+-ATPase was reconstituted into the exogenous lipid DOPC by using a combination of methods from the literature[22,24]with some modifications. Briefly,50mg of DOPC in2ml of buffer(50mM MOPS,0.25M sucrose,1 M KCl,1mM MgCl2,0.1mM CaCl2,1mM DTT,0.025%sodium azide;pH 7.5)containing either of the detergents to give a final lipid:detergent ratio of 1:1.5(w/w)[35]was vortex-mixed vigorously for approximately60s to disperse the lipid and left at room temperature(23-C)for90min.The suspension was clarified by sonication for1À2min with a Soni Prep model 150sonifier/cell disrupter.Purified Ca2+-ATPase was solubilized at a ratio of 0.6:1(w/w;detergent:protein)[35]by vortexing for60s and left at room temperature(23-C)for10min followed by further incubation on ice for an additional90min.The solubilized Ca2+-ATPase was centrifuged at low speed to remove insoluble material and aggregates.The clear sample was then mixed with pre-solubilized exogenous lipid to a desired molar ratio of lipid to Ca2+-ATPase(1500:1)[35],and vortex-mixed for30s and left at room temperature for15min.This mixture was incubated at4-C for90min. At the end of the incubation,the detergent was removed by adsorption on Bio-Beads SM-2in two batches of700mg for1h at4-C.The reconstituted vesicles were separated from the Bio-Beads by low-speed centrifugation.The reconstituted proteoliposomes were purified on a discontinuous sucrose gradient.2.2.8.Assay of Ca2+-ATPase activityCa2+-ATPase activity was determined colorimetrically by measuring Ca2+ dependent release of Pi[2].2.2.9.Simultaneous measurement of Ca2+uptake and ATP hydrolysisSimultaneous measurements of Ca2+uptake and ATP hydrolysis were performed with Fura-Red absorbance continuous spectrophotometric assay as described by Karon et al.[49].All assays were performed at790nM.Ionized free calcium was determined from the equation described by Karon et al.[49] with¨50A g of microsomal protein or¨7A g of reconstituted Ca2+-ATPase preparations with the detergents.2.2.10.Characterization of proteoliposomesThe detergent purified Ca2+-ATPase proteoliposomes were treated with protonophore FCCP(0.25A M)as described by Levy et al.[50]and the Ca2+ uptake studies were performed in presence and absence of the protonophore, FCCP by following the method of Karon et al.[49].2.2.11.Fluorescence spectroscopyFluorescence measurements were made by diluting an aliquot of native microsomes(¨50A g/ml of protein)or purified enzyme with the detergents(¨7 A g protein)into2.5ml of buffer{50mM MOPS,2mM EGTA,pH7.5}.The intrinsic fluorescence of tryptophan was measured with a Perkin Elmer spectrofluorimeter model LS50B.Fluorescence spectra were measured with k ex=295nm and k em=340nm and band widths of4and16nm for excitation and emission,respectively.Fluorescence emission spectra of the E1,E1*Ca and E.Mg states of Ca2+-ATPase in native microsomes and in the purified enzyme preparations were recorded at room temperature(23-C).Ca2+and Mg2+ transitions were induced by adding aliquots of1M of CaCl2and5M of MgCl2 stock solutions to give final concentrations of1mM CaCl2and10mM MgCl2, respectively.The sequential additions were followed at a constant emission wavelength of340nm.2.2.12.Circular dichroismCD measurements were made at room temperature with a Jasco J600 spectropolarimeter with a band width of2nm and a scan speed of2nm/min. Each sample was scanned four times;the scans were automatically averaged. The possible effects of light scattering in the CD measurements were minimized by using a CD cell with a narrow path length(0.1cm)and by using identical concentrations of protein and other experimental parameters for each sample in these comparative studies.2.2.13.Quasi-elastic light scatteringQuasi-elastic light scattering was performed with the Nicomp particle sizer from the Pacific Scientific(Silver Spring,MD,USA)with temperature controlled Peltier heating and cooling as described previously[51]to determine the vesicle size of the native microsomes and the other reconstituted proteoliposomes.2.2.14.Statistical analysisData were analyzed by unpaired t test and analysis of variance, followed by the test of least significant differences for comparisonA.Mandal et al./Biochimica et Biophysica Acta1760(2006)20–31 22within and between the groups.P <0.05was considered as significant [52].3.Results and discussion3.1.Characterization of microsomesWe characterized the microsomal fraction at different steps in the preparation process by measuring the activities of cytochrome c oxidase (a mitochondrial marker)[53],acid phosphatase (a lysosomal marker)[54],rotenone insensitive NADPH-cytochrome c reductase (a microsomal marker)[55]and 5V -nucleotidase (a plasma membrane marker)[54].Microsomal fraction showed,respectively,37-fold decrease in sp.activity of cytochrome c oxidase and 26-fold decrease in the sp.activity of acid phosphatase activity compared with 600–15,000Âg pellet.It also showed 45-fold decrease in sp.activity of 5V -nucleotidase,compared with plasma membrane fraction.Furthermore,the microsomal fraction showed,respec-tively,14-fold and 22-fold increase in the sp.activity of rotenone insensitive NADPH-cytochrome c reductase,com-pared with the 600–15,000Âg pellet and the plasma membrane fraction (Table 1).parison of solubilization of microsomes by DHPC,C 12E 8and Triton X-100Solubilization of membrane proteins by suitable detergents with preservation of native structure and function is important for its detailed biochemical and biophysical studies.The purpose of our present research was to investigate the efficacy of the detergents:Triton X-100,C 12E 8and the short chain phospholipid DHPC to solubilize the microsomes isolated from bovine pulmonary artery smooth muscle tissue for structural and functional studies of Ca 2+-ATPase.DHPC is structurally a phospholipid but its short fatty acid chains of seven carbon atoms endow it with detergent like properties [30].It forms micelles [56]rather than bilayers when dispersed in water with a relatively high c.m.c.of 1.4mM and shows a broad size distribution dependent on its concentration and on the NaCl concentration of the suspension [57].DHPC has the advantage that it is available in pure form,it has no net charge,it is stable over a wide pH range of 4–10,and it does not interfere with spectrophotometric measurements [30,35].Microsomes isolated from bovine pulmonary artery smooth muscle tissue were solubilized with DHPC,C 12E 8and Triton X-100at several concentrations,each ranging from 0to 50Table 1Specific activities of different marker enzymes at different steps in the preparation of microsomes from bovine pulmonary artery smooth muscle tissue FractionCytochrome c oxidase Acidphosphatase Rotenone insensitive NADPH-cytochrome c reductase 5V -Nucleotidase600–15,000g pellet 3.34T 0.21 3.40T 0.230.16T 0.020.18T 0.0315,000–100,000g pellet 0.24T 0.04(7)0.33T 0.05(10) 1.68T 0.12(1050) 2.25T 0.16(1250)Microsomes0.09T 0.01(3)0.13T 0.02(4) 2.20T 0.16(1375)0.07T 0.01(39)Plasma membrane 0.08T 0.01(2)0.14T 0.02(4)0.10T 0.01(63)3.12T 0.20(1733)Cytochrome c oxidase activity is expressed as A mol of cytochrome c utilized/30min/mg protein,acid phosphatase activity as A mol of p -nitrophenol/30min/mg protein,NADPH cytochrome c reductase activity as reduction of absorbance of cytochrome c at 550nm/30min/mg protein and 5V -nucleotidase activity as A mol of P i /30min/mg protein.Results are mean T SE (n =4).Values in the parentheses indicate the activity as percentage of that of the 600–15,000g pellet (values of 600–15,000g pellet are set at100%).Fig.1.Ca 2+-ATPase activity of the supernatant obtained after solubilization of microsomes with several concentrations (0–50mM)of DHPC,C 12E 8and Triton X-100and expressed as percentage of starting microsomal Ca 2+-ATPase activity.Total activity in the supernatant:(),DHPC;(),C 12E 8;(),Triton X-100at various detergent concentration as percentage of starting microsomal Ca 2+-ATPase activity.A.Mandal et al./Biochimica et Biophysica Acta 1760(2006)20–3123mM.To compare the microsome-solubilizing ability of these detergents and Ca 2+-ATPase activity,a percentage of the starting amount of native microsomes was determined in the supernatant of the solubilized membranes after pelleting.The supernatant and the resuspended pelleted materials were treated with Bio-Beads SM-2to remove the detergents present prior to being assayed for the enzyme activity.Phosphatidylcholine (400A g/ml)was added to the resulting sample preparation finally in order to avoid aggregation and denaturation of the enzyme in the assay mixture.Fig.1shows the Ca 2+-ATPase activity recovered from the supernatant of the respective detergent-treated samples.In Fig.1,it appears that significantly more activity is observed upon solubilization by the DHPC over a broad range of DHPC concentration than by the C 12E 8and Triton X-100.Fig.2shows the activity associated with the pelleted fractions of each detergent-treated sample.The sp.activities of these preparations in the soluble fractions are shown in Fig.3as a function of detergent concentration.At very low detergent concentration (5mM),the C 12E 8and Triton X-100solubilized enzyme had a higher sp.activity than that solubilized by DHPC.Above 5mM detergent,however,the sp.activity of the DHPC solubilized Ca 2+-ATPase was significantly greater than that solubilized by any of the other two detergents.Additionally,the C 12E 8and Triton X-100solubilized enzyme rapidly lost theiractivitiesFig.2.Ca 2+-ATPase activity of the pellets obtained after solubilization of microsomes with several concentrations (0–50mM)of DHPC,C 12E 8and Triton X-100and expressed as percentage of starting microsomal Ca 2+-ATPase activity.Total activity in the pellets:(),DHPC;(),C 12E 8;(),Triton X-100atvarious detergent concentration as percentage of starting microsomal Ca 2+-ATPaseactivity.),C 12E 8()and Triton X-100().A.Mandal et al./Biochimica et Biophysica Acta 1760(2006)20–3124with increasing detergent concentration and the optimum range for these detergents is,therefore,very narrow (Fig.3).In contrast,the optimum detergent concentration range for DHPC is relatively broad (Fig.3).The above data for DHPC and C 12E 8support the findings of Shivanna and Rowe [35].It appears that the maximum solubilization as well as the Ca 2+-ATPase activity of the microsomes were obtained with 20mM DHPC,10mM C 12E 8and 10mM Triton X-100(Figs.1–3).3.3.Purification of detergent-solubilized Ca 2+-ATPase The detergent-solubilized preparations were purified by Reactive Red 120-agarose chromatography followed by Sephadex G-100gel filtration.The optimum detergent con-centrations for solubilization of the microsomes were chosen as 20mM for DHPC,10mM for C 12E 8and 10mM for Triton X-100(Figs.1–3).The Ca 2+-ATPase activity-containing frac-tions of the Reactive Red 120-agarose column obtained with 0.5M NaCl were pulled,concentrated and loaded on a Sephadex G-100gel filtration column.The ATPase activity containing fractions of the Sephadex G-100chromatography were eluted between 100and 160ml.The Sephadex G-100purified Ca 2+-ATPase showed a single band ¨115kDa (Fig.4A–C).Furthermore,the immunoblot profile of the purified Ca 2+-ATPase with the detergents indicate that the enzyme migrates with a single band at an apparent molecular mass of ¨115kDa (Fig.4D).The sp.activity of the purified enzyme from the DHPC solubilization was significantly greater than that obtained from the preparation solubilized with C 12E 8and Triton X-100(Table 2).The results of the purification scheme are summarized in Table 2.The sp.activity of the DHPC purified Ca 2+-ATPase is 1.9times greater than that obtained from C 12E 8and 2.2times greater than that obtained with Triton X-100solubilized preparations.These data demonstrate that the DHPC solubili-zation results in a significantly greater quantity of high sp.activity of Ca 2+-ATPase than the other two detergents.The present comparative studies of the result from solubilization and purification of microsomal Ca 2+-ATPase demonstrate the inherent variations exhibited by various detergent groups when interacting with the microsomes.The three detergents employed in this study:DHPC,C 12E 8and Triton X-100represent well-differentiated groups of soluble amphiphiles,i.e.,the phospholipid and non-ionic detergents.The DHPC solubilization consistently provides greater yields,with specific activities significantly greater over a wide concentration range of the detergent than that achieved either by C 12E 8or the Triton X-100(Table 2and Fig.3).The yield of total units of activity at the optimal solubilization concentration for DHPC is 32%and 56%higher than that obtained with C 12E 8and Triton X-100,respectively (Fig.1).CombiningtheFig.4.(A)7.5%SDS-PAGE profile of Ca 2+-ATPase purification with ne 1,microsome;lane 2,DHPC solubilized microsome;lane 3,Reactive Red 120-agarose flow through;lane 4,0.5M NaCl eluate of Reactive Red 120-agarose;lane 5,Sephadex G-100eluate;lane 6,standard mol.wt.markers.(B)7.5%SDS-PAGE profile of Ca 2+-ATPase purification with C 12E ne 1,microsome;lane 2,C 12E 8solubilized microsome;lane 3,Reactive Red 120-agarose flow through;lane 4,0.5M NaCl eluate of Reactive Red 120-agarose;lane 5,Sephadex G-100eluate;lane 6,standard mol.wt.markers.(C)7.5%SDS-PAGE profile of Ca 2+-ATPase purification with Triton ne 1,microsome;lane 2,Triton X-100solubilized microsome;lane 3,Reactive Red 120-agarose flow through;lane 4,0.5M NaCl eluate of Reactive Red 120-agarose;lane 5,Sephadex G-100eluate;lane 6,standard mol.wt.markers.(D)Western blot profile of purified Ca 2+ne 1,control;lane 2,DHPC purified Ca 2+-ATPase;lane 3,C 12E 8purified Ca 2+-ATPase;lane 4,Triton X-100purified Ca 2+-ATPase;lane 5,standard mol.wt.markers.Table 2Purification of Ca 2+-ATPase from bovine pulmonary artery smooth muscle microsomes Purification stepsDetergents used Total protein (mg)Total activity (Units a )Specific activity (Units/mg)Foldpurification Recovery %Microsomes–50745.600.09–100Detergent solubilized microsomesDHPC 53.8830.550.567667C 12E 847.5520.970.441546Triton X-10042.4610.690.252323Reactive Red 120-agarose chromatography DHPC 3.4918.56 5.3185941C 12E 82.969.073.0643420Triton X-100 2.637.31 2.7793116Sephadex G-100chromatographyDHPC 1.38212.378.9519927C 12E 81.320 6.21 4.7045214Triton X-1001.2695.174.0744511aUnit=A mol Pi/min at 37-C.A.Mandal et al./Biochimica et Biophysica Acta 1760(2006)20–3125。

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